US20180355794A1 - A gas turbine system - Google Patents

A gas turbine system Download PDF

Info

Publication number
US20180355794A1
US20180355794A1 US15/777,486 US201615777486A US2018355794A1 US 20180355794 A1 US20180355794 A1 US 20180355794A1 US 201615777486 A US201615777486 A US 201615777486A US 2018355794 A1 US2018355794 A1 US 2018355794A1
Authority
US
United States
Prior art keywords
gas
combustion chamber
ammonia
stream
exhaust gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
US15/777,486
Other versions
US10753276B2 (en
Inventor
Ghenadie Bulat
Timothy Hughes
Jonathan May
Ian Wilkinson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Siemens Energy Global GmbH and Co KG
Original Assignee
Siemens AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Siemens AG filed Critical Siemens AG
Assigned to SIEMENS AKTIENGESELLSCHAFT reassignment SIEMENS AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS PLC
Assigned to SIEMENS AKTIENGESELLSCHAFT reassignment SIEMENS AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED
Assigned to SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED reassignment SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MAY, JONATHAN, MR., BULAT, GHENADIE
Assigned to SIEMENS PLC reassignment SIEMENS PLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: WILKINSON, IAN, MR., HUGHES, TIMOTHY, MR.
Publication of US20180355794A1 publication Critical patent/US20180355794A1/en
Application granted granted Critical
Publication of US10753276B2 publication Critical patent/US10753276B2/en
Assigned to Siemens Energy Global GmbH & Co. KG reassignment Siemens Energy Global GmbH & Co. KG ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS AKTIENGESELLSCHAFT
Active legal-status Critical Current
Adjusted expiration legal-status Critical

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • F02C3/22—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being gaseous at standard temperature and pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • F02C3/26—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being solid or pulverulent, e.g. in slurry or suspension
    • F02C3/28—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being solid or pulverulent, e.g. in slurry or suspension using a separate gas producer for gasifying the fuel before combustion
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
    • C01B3/047—Decomposition of ammonia
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas- turbine plants for special use
    • F02C6/003—Gas-turbine plants with heaters between turbine stages
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23R—GENERATING COMBUSTION PRODUCTS OF HIGH PRESSURE OR HIGH VELOCITY, e.g. GAS-TURBINE COMBUSTION CHAMBERS
    • F23R3/00—Continuous combustion chambers using liquid or gaseous fuel
    • F23R3/28—Continuous combustion chambers using liquid or gaseous fuel characterised by the fuel supply
    • F23R3/36—Supply of different fuels
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/16—Controlling the process
    • C01B2203/1614—Controlling the temperature
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
    • C01B2203/84—Energy production
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2220/00—Application
    • F05D2220/70—Application in combination with
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

  • the present invention relates to combustion of ammonia to release energy.
  • the invention relates to operation of a gas turbine, fuelled by combustion of ammonia.
  • the present invention provides a gas turbine system having a source of ammonia and a source of an oxygen-containing gas, and a first combustion chamber connected to receive three gas streams: ammonia, a hydrogen-rich gas stream and oxygen-containing gas, and a turbine connected to receive an exhaust gas stream from the first combustion chamber.
  • the gas turbine system according to the invention also has a second combustion chamber connected to receive three gas streams: an exhaust gas from the turbine, ammonia and a hydrogen-rich gas stream.
  • the gas turbine system may further have a first cracker chamber that receives ammonia from the ammonia source and to supply a hydrogen-rich gas stream to the first combustion chamber.
  • This hydrogen-rich gas stream supplies the hydrogen required for combustion of ammonia without the need to provide and store hydrogen.
  • the gas turbine system may further have a second cracker chamber arranged to receive ammonia from the ammonia source and to supply a hydrogen-rich gas stream to the second combustion chamber.
  • This hydrogen-rich gas stream supplies the hydrogen required for combustion of ammonia without the need to provide and store hydrogen.
  • a temperature of the, or each, cracker chamber may regulated by mass control of a flow of exhaust gas from the second combustion chamber. This provides temperature control without the need for an external heating source.
  • the gas turbine system may further have a heat exchanger arranged to receive exhaust gas from the second combustion chamber.
  • a steam turbine may be provided, operated by heat derived from the heat exchanger.
  • the present invention also provides a method for combustion of ammonia, including the steps of providing an oxygen-containing gas to a first combustion chamber, providing ammonia to the first combustion chamber; providing a hydrogen-rich gas to the first combustion chamber, performing a first combustion in the first combustion chamber, supplying an exhaust gas from the first combustion chamber to a second combustion chamber, supplying ammonia to the second combustion chamber, supplying a hydrogen-rich gas to the second combustion chamber; and performing a second combustion in the second combustion chamber with an enhanced equivalence ratio.
  • Equivalence ratio in context is the stochiometric ratio.
  • the hydrogen-rich gas supplied to the first combustion chamber is generated by cracking of ammonia.
  • the hydrogen-rich gas supplied to the second combustion chamber may be generated by cracking of ammonia.
  • the cracking may be carried out at an elevated temperature, the elevated temperature being provided by a flow of exhaust gas from the second combustion chamber.
  • the method may further include the step of removing waste heat from exhaust gas stream from the second combustion chamber and recovering energy.
  • the invention also provides a method for extracting energy from ammonia, including performing combustion of ammonia, and including the step of connecting a turbine to receive the exhaust gas from the first combustion chamber and providing exhaust gas from the turbine to the second combustion chamber, the flow of gas through the turbine generating a mechanical output.
  • the single figure schematically illustrates an embodiment of the present invention.
  • the figure shows a gas turbine system according to an exemplary embodiment of the present invention, which includes optional features in addition to the essential features described below.
  • the gas turbine system comprises a source such as compressor 1 which provides an oxygen-containing gas such as air and passes it into a first combustion chamber 2 .
  • Ammonia 3 passes through a calibrated mass flow separator 4 where a portion of the mass flow is passed directly to the first combustion chamber 2 and a second portion is passed to a cracker chamber 5 .
  • the cracker chamber 5 contains a catalyst (Ru, Rh, Pt, Pd or similar) that promotes the decomposition of ammonia NH 3 into a hydrogen-rich gas mixture containing nitrogen, hydrogen and other constituents. The degree of decomposition is controlled by varying the temperature of the ammonia and the catalyst.
  • Elevated temperatures of ammonia and catalyst may be achieved by heat exchange with an exhaust gas flow 20 from a second combustion chamber 7 , to be described below.
  • the elevated temperature may be controlled by varying the mass flow of ammonia through the heat exchanger and mass flow of the exhaust gas 20 through the catalyst bed of the first cracker chamber.
  • Ammonia stream 22 and hydrogen-rich stream 24 are injected into first combustion chamber 2 where combustion takes place producing heat and an exhaust gas flow 26 . Due to incomplete combustion of the ammonia (NH 3 ) the exhaust gas flow will have high levels of NO x .
  • the exhaust gas flow 26 is supplied to a turbine 6 where work is transferred to a shaft or similar, to produce a mechanical output.
  • the exhaust gas flow 26 leaving the turbine is hot and is routed to a second combustion chamber 7 .
  • Ammonia 3 is flowed into a second calibrated flow separator 8 where a portion of the mass flow of ammonia is passed directly to the second combustion chamber 7 as an ammonia stream 28 .
  • a second portion is passed to a second cracker chamber 9 .
  • the cracker chamber 9 contains a catalyst (Ru, Rh, Pt, Pd or similar) that promotes the decomposition of NH 3 into nitrogen, hydrogen and other constituents into a hydrogen-rich stream 30 .
  • the degree of decomposition is controlled by varying the temperature of the gases and catalyst within the second cracker chamber 9 .
  • Elevated temperature in the second cracker chamber 9 may be achieved by heat exchange with an exhaust gas flow 32 from the second combustion chamber 7 .
  • the temperature may be controlled by varying the mass flow of exhaust gas flow 32 through the heat exchanger and mass flow of ammonia through the catalyst bed of the cracker chamber.
  • the ammonia stream 28 and the hydrogen-rich stream 30 are injected into the second combustion chamber 7 where they are combusted.
  • the combustion in the second combustion chamber is performed with an enhanced equivalence ratio typically 1.0-1.2, meaning that an excess of ammonia is present.
  • the enhanced ratio ensures that the combustion produces a significant proportion of NH 2 - ions.
  • the exhaust gas 36 from the 2nd combustion chamber 7 flows through a calibrated flow separator 10 so that a portion of the mass flow is routed to another calibrated flow separator 11 .
  • calibrated flow separators 10 and 11 mass flow is manipulated so that the first and second cracker chambers 5 and 9 are at the required temperatures.
  • a heat exchanger loop 12 is used to remove waste heat from exhaust stream 36 and recover energy, for example by boiling water to rotate a steam turbine 13 .
  • the invention accordingly provides an ammonia-powered turbine, allowing energy stored as ammonia to be recovered into a mechanical output at turbine 6 .
  • nitrogen oxides NOx are removed from the exhaust stream.
  • Combustion in the second combustion chamber is performed at an appropriate equivalence ratio to allow the formation of NH 2 - ions, which combine with NOx in the exhaust gas from the first combustion chamber.
  • the equivalence ratio may be achieved by appropriate selection and control of the temperature of cracker chambers 5 , 9 .
  • the temperature of the cracker chambers may in turn be controlled by controlling the flow of an exhaust gas.
  • the process is energy efficient in that the required heating of cracking chambers to generate a hydrogen-rich stream from ammonia is provided by an exhaust stream from ammonia combustion. This avoids the need for separate provision and storage of a heating source such as hydrogen gas, or provision of heating by other means such as electrical heating.
  • Energy present in the temperature of final exhaust gas may be recovered into mechanical output by operation of a steam turbine or other energy-recovery arrangements.

Abstract

A gas turbine system has a source of ammonia and a source of an oxygen-containing gas, a first combustion chamber connected to receive ammonia, a hydrogen-rich gas stream and oxygen-containing gas, a turbine connected to receive an exhaust gas stream from the first combustion chamber; and a second combustion chamber connected to receive an exhaust gas from the turbine, ammonia and a hydrogen-rich gas stream.

Description

    BACKGROUND OF THE INVENTION Field of the Invention
  • The present invention relates to combustion of ammonia to release energy. In particular, the invention relates to operation of a gas turbine, fuelled by combustion of ammonia.
    • Description of the Prior Art
  • Known procedures for release of energy from ammonia by combustion of the ammonia require supply of ammonia, an oxygen-containing gas and hydrogen. The supply and storage of hydrogen is expensive and raises safety concerns, and the present invention avoids the need to store hydrogen gas. It is preferred to operate the procedure for release of energy from ammonia as efficiently as possible, with minimum waste of energy. It is preferred that no external heat sources or energy sources are required to operate the procedure for combustion of ammonia.
    • SUMMARY OF THE INVENTION
  • The present invention provides a gas turbine system having a source of ammonia and a source of an oxygen-containing gas, and a first combustion chamber connected to receive three gas streams: ammonia, a hydrogen-rich gas stream and oxygen-containing gas, and a turbine connected to receive an exhaust gas stream from the first combustion chamber. The gas turbine system according to the invention also has a second combustion chamber connected to receive three gas streams: an exhaust gas from the turbine, ammonia and a hydrogen-rich gas stream.
  • The gas turbine system may further have a first cracker chamber that receives ammonia from the ammonia source and to supply a hydrogen-rich gas stream to the first combustion chamber. This hydrogen-rich gas stream supplies the hydrogen required for combustion of ammonia without the need to provide and store hydrogen.
  • The gas turbine system may further have a second cracker chamber arranged to receive ammonia from the ammonia source and to supply a hydrogen-rich gas stream to the second combustion chamber. This hydrogen-rich gas stream supplies the hydrogen required for combustion of ammonia without the need to provide and store hydrogen.
  • A temperature of the, or each, cracker chamber may regulated by mass control of a flow of exhaust gas from the second combustion chamber. This provides temperature control without the need for an external heating source.
  • The gas turbine system may further have a heat exchanger arranged to receive exhaust gas from the second combustion chamber. A steam turbine may be provided, operated by heat derived from the heat exchanger.
  • The present invention also provides a method for combustion of ammonia, including the steps of providing an oxygen-containing gas to a first combustion chamber, providing ammonia to the first combustion chamber; providing a hydrogen-rich gas to the first combustion chamber, performing a first combustion in the first combustion chamber, supplying an exhaust gas from the first combustion chamber to a second combustion chamber, supplying ammonia to the second combustion chamber, supplying a hydrogen-rich gas to the second combustion chamber; and performing a second combustion in the second combustion chamber with an enhanced equivalence ratio. Equivalence ratio in context is the stochiometric ratio.
  • The hydrogen-rich gas supplied to the first combustion chamber is generated by cracking of ammonia.
  • The hydrogen-rich gas supplied to the second combustion chamber may be generated by cracking of ammonia.
  • The cracking may be carried out at an elevated temperature, the elevated temperature being provided by a flow of exhaust gas from the second combustion chamber.
  • The method may further include the step of removing waste heat from exhaust gas stream from the second combustion chamber and recovering energy.
  • The invention also provides a method for extracting energy from ammonia, including performing combustion of ammonia, and including the step of connecting a turbine to receive the exhaust gas from the first combustion chamber and providing exhaust gas from the turbine to the second combustion chamber, the flow of gas through the turbine generating a mechanical output.
    • BRIEF DESCRIPTION OF THE DRAWINGS
  • The single figure schematically illustrates an embodiment of the present invention.
    •  DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • The figure shows a gas turbine system according to an exemplary embodiment of the present invention, which includes optional features in addition to the essential features described below.
  • In the illustrated embodiment, the gas turbine system comprises a source such as compressor 1 which provides an oxygen-containing gas such as air and passes it into a first combustion chamber 2. Ammonia 3 passes through a calibrated mass flow separator 4 where a portion of the mass flow is passed directly to the first combustion chamber 2 and a second portion is passed to a cracker chamber 5. The cracker chamber 5 contains a catalyst (Ru, Rh, Pt, Pd or similar) that promotes the decomposition of ammonia NH3 into a hydrogen-rich gas mixture containing nitrogen, hydrogen and other constituents. The degree of decomposition is controlled by varying the temperature of the ammonia and the catalyst. Elevated temperatures of ammonia and catalyst may be achieved by heat exchange with an exhaust gas flow 20 from a second combustion chamber 7, to be described below. The elevated temperature may be controlled by varying the mass flow of ammonia through the heat exchanger and mass flow of the exhaust gas 20 through the catalyst bed of the first cracker chamber.
  • Ammonia stream 22 and hydrogen-rich stream 24 are injected into first combustion chamber 2 where combustion takes place producing heat and an exhaust gas flow 26. Due to incomplete combustion of the ammonia (NH3) the exhaust gas flow will have high levels of NOx. The exhaust gas flow 26 is supplied to a turbine 6 where work is transferred to a shaft or similar, to produce a mechanical output.
  • The exhaust gas flow 26 leaving the turbine is hot and is routed to a second combustion chamber 7. Ammonia 3 is flowed into a second calibrated flow separator 8 where a portion of the mass flow of ammonia is passed directly to the second combustion chamber 7 as an ammonia stream 28. A second portion is passed to a second cracker chamber 9. The cracker chamber 9 contains a catalyst (Ru, Rh, Pt, Pd or similar) that promotes the decomposition of NH3 into nitrogen, hydrogen and other constituents into a hydrogen-rich stream 30. The degree of decomposition is controlled by varying the temperature of the gases and catalyst within the second cracker chamber 9. Elevated temperature in the second cracker chamber 9 may be achieved by heat exchange with an exhaust gas flow 32 from the second combustion chamber 7. The temperature may be controlled by varying the mass flow of exhaust gas flow 32 through the heat exchanger and mass flow of ammonia through the catalyst bed of the cracker chamber.
  • The ammonia stream 28 and the hydrogen-rich stream 30 are injected into the second combustion chamber 7 where they are combusted. The combustion in the second combustion chamber is performed with an enhanced equivalence ratio typically 1.0-1.2, meaning that an excess of ammonia is present. The enhanced ratio ensures that the combustion produces a significant proportion of NH2- ions. These NH2- ions combine with the NOx in the exhaust stream 34 from the turbine 6 to produce N2 and H2O, thereby removing the NOx from the exhaust stream.
  • The exhaust gas 36 from the 2nd combustion chamber 7 flows through a calibrated flow separator 10 so that a portion of the mass flow is routed to another calibrated flow separator 11. By control of calibrated flow separators 10 and 11, mass flow is manipulated so that the first and second cracker chambers 5 and 9 are at the required temperatures.
  • Preferably, a heat exchanger loop 12 is used to remove waste heat from exhaust stream 36 and recover energy, for example by boiling water to rotate a steam turbine 13.
  • The invention accordingly provides an ammonia-powered turbine, allowing energy stored as ammonia to be recovered into a mechanical output at turbine 6.
  • By use of dual combustion chambers, nitrogen oxides NOx are removed from the exhaust stream. Combustion in the second combustion chamber is performed at an appropriate equivalence ratio to allow the formation of NH2- ions, which combine with NOx in the exhaust gas from the first combustion chamber. The equivalence ratio may be achieved by appropriate selection and control of the temperature of cracker chambers 5, 9.
  • The temperature of the cracker chambers may in turn be controlled by controlling the flow of an exhaust gas.
  • The process is energy efficient in that the required heating of cracking chambers to generate a hydrogen-rich stream from ammonia is provided by an exhaust stream from ammonia combustion. This avoids the need for separate provision and storage of a heating source such as hydrogen gas, or provision of heating by other means such as electrical heating.
  • Energy present in the temperature of final exhaust gas may be recovered into mechanical output by operation of a steam turbine or other energy-recovery arrangements.
  • Although modifications and changes may be suggested by those skilled in the art, it is the intention of the Applicant to embody within the patent warranted hereon all changes and modifications as reasonably and properly come within the scope of the Applicant's contribution to the art.

Claims (11)

1-16. (canceled)
17. A gas turbine system comprising:
a source of ammonia and a source of an oxygen-containing gas;
a first combustion chamber connected to receive a stream of ammonia gas, a gas stream comprising hydrogen gas, and an oxygen-containing gas;
a turbine connected to receive an exhaust gas stream from the first combustion chamber;
a second combustion chamber connected to receive an exhaust gas from the turbine, a stream of ammonia gas, and a gas stream comprising hydrogen gas;
a source of ammonia connected to the first combustion chamber and providing the stream of ammonia gas to the first combustion chamber;
said source of ammonia also being connected to the second combustion chamber and providing the stream of ammonia gas to the second combustion chamber; and
a first cracker chamber arranged to receive ammonia gas from the source of ammonia gas and to supply the gas stream comprising hydrogen gas to the first combustion chamber.
18. A gas turbine system as claimed in claim 17 further comprising a second cracker chamber arranged to receive ammonia gas from the ammonia gas source and to supply the gas stream comprising hydrogen gas to the second combustion chamber.
19. A gas turbine system as claimed in claim 18 wherein a temperature of at least one of said first cracker chamber and said second cracker chamber is regulated by mass control of a flow of exhaust gas from the second combustion chamber.
20. A gas turbine system as claimed in claim 17 further comprising a heat exchanger arranged to receive exhaust gas from the second combustion chamber.
21. A gas turbine system as claimed in claim 20 comprising a steam turbine operated by heat derived from said heat exchanger.
22. A method for extracting energy from ammonia, comprising the steps of:
providing an oxygen-containing gas to a first combustion chamber;
providing ammonia to the first combustion chamber;
providing a gas stream comprising hydrogen gas to the first combustion chamber;
performing a first combustion in the first combustion chamber that produces an exhaust gas;
providing said exhaust gas from said first combustion chamber to a second combustion chamber;
supplying ammonia to the second combustion chamber;
supplying a stream comprising hydrogen gas to the second combustion chamber;
performing a second combustion in the second combustion chamber with an enhanced equivalence ratio;
generating the gas stream comprising hydrogen gas, which is supplied through the first combustion chamber, by tracking of ammonia; and
connecting a turbine to receive the exhaust gas from the first combustion chamber and providing exhaust gas from the turbine to the second combustion chamber and thereby causing a flow of gas through the combustion to generate a mechanical output.
23. A method for extracting energy from ammonia as claimed in claim 22 wherein said equivalence ratio is in a range between 1.0 and 1.2.
24. A method as claimed in claim 22 comprising generating the gas stream comprising hydrogen gas to the second combustion chamber by cracking of ammonia.
25. A method as claimed in claim 24 comprising conducting said cracking of ammonia at an elevated temperature provided by a flow of exhaust gas from the second combustion chamber.
26. A method as claimed in claim 22 comprising removing waste heat from an exhaust gas stream from the second combustion chamber, and recovering energy from said waste heat.
US15/777,486 2015-11-20 2016-11-02 Gas turbine system Active 2037-06-30 US10753276B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB1520612.1A GB2544552A (en) 2015-11-20 2015-11-20 A gas turbine system
GB1520612.1 2015-11-20
PCT/EP2016/076453 WO2017084876A1 (en) 2015-11-20 2016-11-02 A gas turbine system

Publications (2)

Publication Number Publication Date
US20180355794A1 true US20180355794A1 (en) 2018-12-13
US10753276B2 US10753276B2 (en) 2020-08-25

Family

ID=55133209

Family Applications (1)

Application Number Title Priority Date Filing Date
US15/777,486 Active 2037-06-30 US10753276B2 (en) 2015-11-20 2016-11-02 Gas turbine system

Country Status (9)

Country Link
US (1) US10753276B2 (en)
EP (1) EP3377745B1 (en)
JP (1) JP6779998B2 (en)
KR (1) KR102622896B1 (en)
CN (1) CN108350806B (en)
AU (1) AU2016356598B2 (en)
CA (1) CA3001942C (en)
GB (1) GB2544552A (en)
WO (1) WO2017084876A1 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11156168B2 (en) * 2016-11-08 2021-10-26 Mitsubishi Power, Ltd. Gas turbine plant having thermal decomposition of ammonia and pressurization of the decomposed gas and method thereof
US20220195919A1 (en) * 2020-12-18 2022-06-23 New Wave Hydrogen, Inc. Zero-Emission Jet Engine Employing A Dual-Fuel Mix Of Ammonia And Hydrogen Using A Wave
US11649762B2 (en) * 2020-05-06 2023-05-16 New Wave Hydrogen, Inc. Gas turbine power generation systems using hydrogen-containing fuel produced by a wave reformer and methods of operating such systems
EP4230847A1 (en) * 2022-02-15 2023-08-23 Doosan Enerbility Co., Ltd. Combined power generation system and driving method thereof
US11890611B2 (en) 2021-04-27 2024-02-06 New Wave Hydrogen, Inc. Conversion system for wave-rotor reactor system

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3450850A1 (en) * 2017-09-05 2019-03-06 Siemens Aktiengesellschaft A gas turbine combustor assembly with a trapped vortex cavity
AU2018377847A1 (en) * 2017-11-28 2020-06-11 Renam Properties Pty Ltd Autonomous vehicle energy and service hub
US11920524B2 (en) * 2021-04-15 2024-03-05 Rtx Corporation Multi-fuel, fuel injection system for a turbine engine
KR102536353B1 (en) * 2021-10-27 2023-05-26 두산에너빌리티 주식회사 Combined power plant and operating method of the same
WO2023144335A1 (en) * 2022-01-27 2023-08-03 Thyssenkrupp Industrial Solutions Ag Process and plant for producing hydrogen from ammonia
GB202210681D0 (en) * 2022-07-21 2022-09-07 Johnson Matthey Plc Process
KR20240033947A (en) 2022-09-06 2024-03-13 한국에너지기술연구원 Production apparatus and method for high purity hydrogen using ammonia
EP4361096A1 (en) 2022-10-24 2024-05-01 Linde GmbH Method and apparatus for processing ammonia
EP4361094A1 (en) 2022-10-24 2024-05-01 Linde GmbH Method and apparatus for processing ammonia
EP4361095A1 (en) 2022-10-24 2024-05-01 Linde GmbH Method and apparatus for providing heat
WO2024090092A1 (en) * 2022-10-28 2024-05-02 株式会社Ihi Combustion system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3313103A (en) * 1965-08-25 1967-04-11 Gen Motors Corp Gas turbine combustion process
US20090133400A1 (en) * 2007-11-28 2009-05-28 Caterpillar Inc. Turbine engine having fuel-cooled air intercooling
US20120047870A1 (en) * 2009-01-14 2012-03-01 Toyota Jidosha Kabushiki Kaisha Engine

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2297186A1 (en) * 1975-01-10 1976-08-06 Peauroux Bernard METHOD AND DEVICE FOR DISSOCIATION OF AMMONIAC GAS, WITH A VIEW, IN PARTICULAR, OF ITS USE FOR SUPPLYING THERMAL ENGINES
GB1537109A (en) * 1975-10-23 1978-12-29 Gen Electric Gas turbine combustion system
EP0317110B1 (en) * 1987-11-18 1992-03-04 Radian Corporation Low nox cogeneration process
JP2948351B2 (en) 1991-05-17 1999-09-13 三菱重工業株式会社 Turbine plant
EP0523469A1 (en) * 1991-07-18 1993-01-20 Siemens Aktiengesellschaft Method for the reduction of NOx emission of a gas turbine
WO2001087770A1 (en) * 2000-05-12 2001-11-22 Gradient Technology Production of hydrogen by autothermic decomposition of ammonia
GB0509163D0 (en) * 2005-05-05 2005-06-15 Boc Group Plc Gas combustion apparatus
DE102008054038B3 (en) * 2008-10-30 2010-04-29 Karlsruher Institut für Technologie Method and device for reducing pollutant emissions in incinerators
JP5049947B2 (en) * 2008-11-19 2012-10-17 日立造船株式会社 Ammonia engine system
CN101538010B (en) 2009-03-17 2011-04-06 陈效刚 System for decomposing ammonia to prepare hydrogen on the basis of after heat of heat engine gas exhaust
TWI593878B (en) * 2010-07-02 2017-08-01 艾克頌美孚上游研究公司 Systems and methods for controlling combustion of a fuel
JP2012255420A (en) * 2011-06-10 2012-12-27 Nippon Shokubai Co Ltd Gas turbine system
US20130269356A1 (en) * 2012-04-12 2013-10-17 General Electric Company Method and system for controlling a stoichiometric egr system on a regenerative reheat system
JP5935124B2 (en) * 2012-11-12 2016-06-15 一般財団法人電力中央研究所 Turbine equipment and power generation equipment
JP5900972B2 (en) * 2013-03-22 2016-04-06 一般財団法人電力中央研究所 NH3 cogeneration plant
JP6153163B2 (en) * 2013-08-02 2017-06-28 一般財団法人電力中央研究所 Reheat type ammonia gas turbine
JP2015190466A (en) 2014-03-31 2015-11-02 株式会社Ihi Combustion device, gas turbine and power generation device
GB2539667B (en) 2015-06-23 2018-04-04 Siemens Ag Method and equipment for combustion of ammonia

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3313103A (en) * 1965-08-25 1967-04-11 Gen Motors Corp Gas turbine combustion process
US20090133400A1 (en) * 2007-11-28 2009-05-28 Caterpillar Inc. Turbine engine having fuel-cooled air intercooling
US20120047870A1 (en) * 2009-01-14 2012-03-01 Toyota Jidosha Kabushiki Kaisha Engine

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11156168B2 (en) * 2016-11-08 2021-10-26 Mitsubishi Power, Ltd. Gas turbine plant having thermal decomposition of ammonia and pressurization of the decomposed gas and method thereof
US11649762B2 (en) * 2020-05-06 2023-05-16 New Wave Hydrogen, Inc. Gas turbine power generation systems using hydrogen-containing fuel produced by a wave reformer and methods of operating such systems
US20220195919A1 (en) * 2020-12-18 2022-06-23 New Wave Hydrogen, Inc. Zero-Emission Jet Engine Employing A Dual-Fuel Mix Of Ammonia And Hydrogen Using A Wave
US11773777B2 (en) * 2020-12-18 2023-10-03 New Wave Hydrogen, Inc. Zero-emission jet engine employing a dual-fuel mix of ammonia and hydrogen using a wave
US11890611B2 (en) 2021-04-27 2024-02-06 New Wave Hydrogen, Inc. Conversion system for wave-rotor reactor system
EP4230847A1 (en) * 2022-02-15 2023-08-23 Doosan Enerbility Co., Ltd. Combined power generation system and driving method thereof
US11905855B2 (en) 2022-02-15 2024-02-20 Doosan Enerbility Co., Ltd. Combined power generation system and driving method thereof

Also Published As

Publication number Publication date
JP6779998B2 (en) 2020-11-04
KR102622896B1 (en) 2024-01-08
CN108350806B (en) 2023-05-26
JP2018535355A (en) 2018-11-29
AU2016356598B2 (en) 2020-09-10
EP3377745B1 (en) 2019-08-21
KR20180084051A (en) 2018-07-24
WO2017084876A1 (en) 2017-05-26
AU2016356598A1 (en) 2018-04-26
CA3001942C (en) 2023-12-19
CA3001942A1 (en) 2017-05-26
CN108350806A (en) 2018-07-31
GB201520612D0 (en) 2016-01-06
GB2544552A (en) 2017-05-24
US10753276B2 (en) 2020-08-25
EP3377745A1 (en) 2018-09-26

Similar Documents

Publication Publication Date Title
US10753276B2 (en) Gas turbine system
US20240125270A1 (en) Systems and methods for power production with integrated production of hydrogen
CN107810365B (en) Method and apparatus for burning ammonia
US8850787B2 (en) Hybrid thermal power generation system and method of constructing same
NO330544B1 (en) Procedure for operating a power plant with a substantially closed CO2 process as well as a power plant with such a process
US20140377157A1 (en) Method and device for producing nitric acid
KR102096259B1 (en) Methods and equipment for the combustion of ammonia
MX2014007408A (en) Multistage method for producing a hydrogen-containing gaseous fuel and thermal gas generator plant.
US20120285175A1 (en) Steam injected gas turbine engine
JP2002241101A (en) System and method for hydrogen generation using atomic reactor
KR101511100B1 (en) System and method of fuel cell power generation by using exhaust gas of high temperature from fuel cell power generation system
KR102101178B1 (en) Method for operating a gas and steam combined cycle power plant
JP2001271610A (en) Co2 recovery gas turbine system
JP2005337214A (en) Heavy oil reforming gas turbine power generation system using high temperature/high pressure water
JP2006312917A (en) Power generating facility, gas turbine power generating facility, reformed fuel supplying method for power generating facility
JP2023084456A (en) Chemical synthesis system and chemical synthesis method
JP2017535706A (en) Methods and equipment for simultaneous generation of mechanical power and production of hydrocarbons

Legal Events

Date Code Title Description
FEPP Fee payment procedure

Free format text: ENTITY STATUS SET TO UNDISCOUNTED (ORIGINAL EVENT CODE: BIG.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

AS Assignment

Owner name: SIEMENS AKTIENGESELLSCHAFT, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SIEMENS PLC;REEL/FRAME:047696/0577

Effective date: 20181030

Owner name: SIEMENS PLC, UNITED KINGDOM

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:HUGHES, TIMOTHY, MR.;WILKINSON, IAN, MR.;SIGNING DATES FROM 20180708 TO 20181017;REEL/FRAME:047695/0786

Owner name: SIEMENS AKTIENGESELLSCHAFT, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED;REEL/FRAME:047696/0494

Effective date: 20180619

Owner name: SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED, UNITED

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BULAT, GHENADIE;MAY, JONATHAN, MR.;SIGNING DATES FROM 20180522 TO 20180611;REEL/FRAME:047696/0387

Owner name: SIEMENS INDUSTRIAL TURBOMACHINERY LIMITED, UNITED KINGDOM

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:BULAT, GHENADIE;MAY, JONATHAN, MR.;SIGNING DATES FROM 20180522 TO 20180611;REEL/FRAME:047696/0387

STPP Information on status: patent application and granting procedure in general

Free format text: NOTICE OF ALLOWANCE MAILED -- APPLICATION RECEIVED IN OFFICE OF PUBLICATIONS

STPP Information on status: patent application and granting procedure in general

Free format text: NOTICE OF ALLOWANCE MAILED -- APPLICATION RECEIVED IN OFFICE OF PUBLICATIONS

STPP Information on status: patent application and granting procedure in general

Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT VERIFIED

STCF Information on status: patent grant

Free format text: PATENTED CASE

AS Assignment

Owner name: SIEMENS ENERGY GLOBAL GMBH & CO. KG, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SIEMENS AKTIENGESELLSCHAFT;REEL/FRAME:056501/0020

Effective date: 20210228

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 4TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1551); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 4